Multilayer heat shrinkable cook-in film

ABSTRACT

The present invention is directed to a cook-in film and to bags, pouches and the like made therefrom. The invention is further directed to a method of producing and preserving a food product using such a film, bag or pouche and to a packaged food product obtained therefrom.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application claims the benefit of European Application No. 07108945.2, filed May 25, 2007, the entire disclosure of which is herein incorporated by reference.

TECHNICAL FIELD

The present invention is directed to a cook-in film and to bags, pouches and the like made therefrom. The invention is further directed to a method of producing and preserving a food product using such a film, bag or pouche and to a packaged food product obtained therefrom.

BACKGROUND

Many food products are processed in thermoplastic film packages by subjecting the packed product to elevated temperatures produced by, for example, exposure to steam, hot air or immersion into boiling water. This thermal processing is usually called cook-in and the films used for such applications are generally called cook-in films.

A cook-in film must be capable of withstanding exposure to severe temperature conditions like immersion in hot water of a temperature of 70 to 90° C. for a time period of about 4 to 18 hours. During these severe thermal conditions, the film should be able to withstand

-   -   1. Opening of the seals     -   2. Delamination of the different layers of the multilayer         structure.

A further desirable effect of the cook-in films is heat shrinkability, which is the ability of a film to shrink under heat conditions so that it conforms tightly to the packed food and gives a good aesthetic appearance.

A further desirable effect is good optical properties, meaning high gloss and low haze of the film, providing a nice presentation to the consumer.

Another desirable effect is the ability of the film to heat seal effectively in commercial bag making machines. The reason for this is that very often, the film is used in the form of a bag (pouch) in which the product is packed under vacuum and then is put in a hot water bath or in a steam container in order to be cooked.

Still another desirable effect is high heat seal strength not only after the heat treatment (cook-in or post pasteurization process) but also before.

Thus, it would be desirable to make a heat shrinkable film combining all these different requirements

1. Resistance to bag opening and delamination 2. High shrinkage 3. Excellent optics 4. Efficient heat sealability

It is also known in the art a similar process called post pasteurization. Many foods require pasteurization after being hermetically packed so that harmful microbes are destroyed. Specific pasteurization requirements may vary from country to country but 1 hour at 95° C. is considered a possible limiting case. The film of the invention may be used also to withstand these conditions.

In the prior art, often polypropylene copolymers have been proposed to be used in cook-in applications. These copolymers generally offer high resistance of the seals after the thermal treatment process. But because of their stiff nature, PP polymers often have weak seals during loading filling process that is before the cook-in process. In the real market conditions this weakness may result in many failures of the seals especially in cases where the loaded items are heavy.

SUMMARY OF THE INVENTION

It is, therefore, an object of the present invention to provide a heat shrinkable multilayer film having excellent optics, efficient heat sealability, resistance to bag opening and delamination, and sealstrength during loading. It is a further object of the present invention to provide a cook-in film having the above properties.

These objects are achieved by the subject-matter of the independent claims. Preferred embodiments are set forth in the dependent claims.

The invention is based on the surprising insight that multilayer films for high temperature applications (up to about 95° C.; so called cook-in films) may be produced by introducing a heat sealing layer comprising an olefin block copolymer.

It surprisingly turned out that the multilayer films of the present invention remained stable under these circumstances, i.e. did not show opening of the seals and delamination. Moreover, the multilayer film of the invention showed an improved heat sealability due to using an inner heat sealing layer having the above properties.

Thus, a very stable multilayer film for cook-in applications could be generated having improved characteristics regarding opening of the seals and delamination, but also regarding heat-shrinkability.

Briefly the invention provides an oriented heat shrinkable film comprising a heat sealing layer comprising an olefin block polymer. Other layers may include an oxygen barrier layer and an outer layer comprising polyolefin polymer or styrene butadiene copolymer.

The definitions used in the following are as follows:

The term “film” refers to a flat or tubular flexible structure of thermoplastic material. A “cook-in film” is more specifically defined as being a film adapted for high temperature applications, e.g. treatment with hot water at temperatures between about 70°-98° C., e.g. up to about 95° C. The time period for subjecting the packaged food product to the elevated temperature is between about 1-18 hours.

The term “heat shrinkable” refers to a film that shrinks at least 10% in at least one of the longitudinal and transverse directions when heated at 90° C. for 4 seconds. The shrinkability is measured according to ASTM 2732. This test method covers the determination of the degree of unrestrained linear thermal shrinkage at given specimen temperatures of a plastic film and sheeting of 0.76 mm thickness or less.

For the determination of the melting point, the instrumental method used is DSC (differential scanning calorimetry) in accordance with ASTM D 3418.

All measurement methods mentioned herein are readily available for the skilled person. For example, they can be obtained from the American National Standards Institute at: www.webstore.ansi.org

The phrase “longitudinal direction” or “machine direction” herein abbreviated “MD” refers to a direction along the length of the film.

The phrase “outside layer” refers to the film layer which comes in immediate contact with the outside environment (atmosphere).

The phrase “inner layer” refers to the film layer that comes in direct contact with the product packed. This is also called “sealing layer” as this layer must be hermetically sealed in order to protect the product from ingress of air.

The term “barrier layer” is the layer providing protection against oxygen coming into the package from the atmosphere. Suitable materials are PVDC, EVOH, polyamide etc.

As used herein, the term “homopolymer” refers to a polymer resulting from polymerization of a single monomer.

As used herein, the term “copolymer” refers to a polymer resulting from polymerization of at least two different polymers.

As used herein, the term “polymer” includes both above types.

As used herein the term “polyethylene” identifies polymers consisting essentially of the ethylene repeating unit. The ones that have a density more than 0.940 are called high density polyethylene (HDPE), the ones that are have less than 0.940 are low density polyethylene (LDPE).

As used herein the phrase “ethylene alpha olefin copolymer” refers to polymers like linear low density polyethylene (LLDPE), medium density polyethylene (MDPE), very low density polyethylene (VLDPE), ultra low density polyethylene (ULDPE), metallocene catalysed polymers and polyethylene plastomers and elastomers.

As used herein the phrase “styrene polymers” refers to styrene homopolymer such as polystyrene and to styrene copolymers such as styrene-butadiene copolymers, styrene-butadiene-styrene copolymers, styrene-isoprene-styrene copolymers, styrene-ethylene-butadiene-styrene copolymers, ethylene-styrene copolymers and the like.

As used herein the phrase “ethylene methacrylate copolymers” refers to copolymers of ethylene and methacrylate monomer. The monomer content is preferably less than 40 wt.-%.

As used herein the phrase “ethylene vinyl acetate copolymer” refer to copolymers of ethylene and vinyl acetate.

As used herein, the term EVOH refers to saponified products of ethylene vinyl ester copolymers. The ethylene content is typically in the range of 25 to 50 wt.-%.

As used herein the term PVDC refers to a vinylidene chloride copolymer wherein a major amount of the copolymer comprises vinylidene chloride and a minor amount of the copolymer comprises one or more monomers such as vinyl chloride and/or alkyl acrylates and methacrylates.

As used herein the term polyamide refers to homopolymers and copolymers.

As used herein the term “polypropylene” refers to any homopolymer, copolymer, terpolymer, tetrapolymer etc. that includes mer units of propylene. The term as used in the present application includes homopolymers, random copolymers, propylene alpha olefin copolymers, propylene ethylene copolymers propylene-ethylene-alpha olefin copolymers and other propylene polymers.

As used herein the term “ethylene alpha olefin block copolymer” refers to copolymer comprising hard and soft blocks. Each of hard and soft blocks comprise a copolymer of ethylene and alpha olefin, like propylene, butane, hexane, octene. Typical polymers are described in applications US 20030073785, JP-A-60/35009, US 2006/0199030. Preferably, the molecular weight distribution of the olefin block copolymer is between 1.2 and 3.5.

DETAILED DESCRIPTION

According to a first aspect, the present invention provides a heat shrinkable film comprising a heat sealing layer comprising an ethylene olefin block copolymer.

More precisely, the heat sealing layer of the multilayer film of the present invention comprises an ethylene octene block copolymer having a melting point of more than 115° C.

In another aspect of the invention, next to the sealing layer there is a layer comprising polypropylene.

PP might be present as a heterogeneous or a homogeneous polymer produced with single site catalyst. It may also be a blend of such a material with the following

-   -   1. another PP polymer such as random copolymer or homopolymer         (among others)     -   2. a polyethylene polymer such as an alpha olefin copolymer with         density 0.860 to about 0.960 or such as an ethylene ester         copolymer     -   3. a cyclic olefin copolymer     -   4. a styrene polymer     -   5. an ionomer or a methacrylic acid copolymer     -   6. polybutene polymer

In another preferred case, the PP polymer may be blended with an ethylene alpha olefin copolymer which has a vicat softening point less than 100° C.

Examples of polymers that could be useful are

-   -   Homogeneous ethylene alpha olefin copolymers like the EXACT         grades from EXXON;     -   Homogeneous ethylene alpha olefin copolymers with long chain         branching such as the AFFINITY grades from DOW;     -   TAFMER linear ethylene alpha olefin copolymers from MITSUI.

The oxygen barrier layer used may include a high oxygen barrier material such as a polyvinylidene chloride homopolymer or copolymer or an ethylene vinyl alcohol copolymer (EVOH). Other oxygen barrier materials are also well known in the art. As example, oxygen barrier materials, also polyamides or polyesters may be used.

In the outside layer the following materials may be used

-   -   1. a polypropylene homopolymer or copolymer having a vicat         softening point of less than 105° C. measured under ASTM D 1525.         It is preferably a homogeneous polymer produced with single site         catalyst,     -   2. PP polymer such as random copolymer or homopolymer (among         others)     -   3. Polyethylene polymer such as an alpha olefin copolymer with         density 0.860 to about 0.960 or such as an ethylene ester         copolymer     -   4. a cyclic olefin copolymer     -   5. a styrene polymer     -   6. a ionomer or a methacrylic acid copolymer.

A preferred version comprises a

1. styrene butadiene copolymer 2. a blend of styrene butadiene copolymer and an ethylene alpha olefin copolymer 3. a reactor made TPO polymer incorporating propylene mer units 4. a blend of a reactor made TPO polymer incorporating propylene mer units and polypropylene homopolymer or copolymer 5. a propylene ethylene polymer with a vicat softening point less than 100° C. 6. a blend of two propylene ethylene polymers with a vicat softening point less than 100° C. 7. further preferred is a film which comprises an outside layer incorporating

-   -   a polypropylene polymer     -   an ethylene alpha olefin copolymer     -   a styrene butadiene polymer     -   a polyamide     -   a polybutene or     -   an EVOH polymer or a combination of one or more thereof.

Between the inner heat sealing layer and the oxygen barrier layer may exist further layers that could comprise any of the polymers mentioned in the possibilities for inner heat sealing layer. Preferred materials are ethylene vinyl acetate, ethylene alpha olefin copolymers, EMA polymers, polypropylene copolymers, polybutylene, styrene homopolymers or copolymers.

Between the outer layer and the oxygen barrier layer may exist further layers that could comprise any of the polymers mentioned in the possibilities for inner heat sealing layer. Preferred materials are ethylene vinyl acetate, ethylene alpha olefin copolymers, EMA polymers, polypropylene copolymers, polybutylene, styrene homopolymers or copolymers.

Any of the layers described above may also include additives well known in the art such as slip agents, antiblock, polymer processing aids, antistatic, antifog, acid scavengers, odour scavengers and the like. A person skilled in the art may select the right additives according to any particular needs.

In a preferred version of the application, the film is irradiated with e beam radiation of levels from 1 to 10 MRAD.

All the percentages indicated in this application are per weight except if differently stated.

EXAMPLES Example 1

A 5 layer film is produced in a double bubble (the double bubble method is described in U.S. Pat. No. 3,456,044, incorporated herein by reference) commercial line with the following structure:

Inner (sealing) layer, 100% EOB1 Adjacent layer 93% E1 + 7% ADDITIVES Barrier layer PVDC commercial grade Adjacent layer 30% M1 + 65% E2 + 5% ADDITIVES Outer layer 100% EAO1 See table 1, 2

Example 2

A 5 layer film is produced in a double bubble (the double bubble method is described in U.S. Pat. No. 3,456,044) commercial line with the following recipe

Inner (sealing layer), 100% EOB2 Adjacent layer 93% E1 + 7% ADDITIVES Barrier layer PVDC commercial grade Adjacent layer 30% M1 + 65% E2 + 5% ADDITIVES Outer layer 100% S1

In all the above examples, the thickness of the layers are (in microns)

-   8, outer layer -   10, adjacent layer -   4, barrier layer -   6, adjacent layer -   27, heat sealing layer

Comparative Example

Under exactly the same conditions a commercial product FMXBK was produced.

All the samples were e-beam radiated with a dose of 4 MRAD prior to bag making.

TABLE 1 Melt Melting Index Density point Type Description Manufacturer g/10 min g/cm³ ° C. E1 EVA Dupont 3135 X 0.35 0.93 95 E2 EVA Dupont 3165 0.7 0.94 89 S1 SB DK13 10 1.01 COPOLYMER M1 EMA ARKEMA 2-3.5 0.95 61 copolymer LOTRYL 29MAO3 EOB1 Ethylene 0.87 121 octene block copolymer EOB2 Ethylene 0.88 octene block copolymer EOA1 Ethylene Dow PL 1880 1 0.902 100 octene random homogenous copolymer

TABLE 2 HAZE GLOSS SHRINKAGE(MD/TD) Example 1 9 102 35/35 Example 2 7 110 38/37 Comparison 7 100 32/35

For better evaluation of the resistance of the sealing properties under cook-in conditions, the following experiment was executed.

Material from samples 1-2 and comparative sample were made into bag configuration in a pouch making machine. Then the bags were filled with water and sealed at the open end. Then the bags were put in a hot water bath and cooked at 95° C. for 5 hours. After this thermal treatment, the bags were examined if their seals were destroyed and if delamination was noticed.

TABLE 3 Results of cook-in test Example 1 No bag opened Example 2 No bag opened Comparison No bag opened

Haze is measured according to ASTM D 1003, gloss according to BS 2782 and shrinkage according to ASTM 2732.

Test for Evaluation of Seal Strength

A bag is clamped at its two edges. A falling weight of 2 kilos is thrown on the interior of the bag from a height of 1.5 meters. Percentage of opened bags is calculated. The results for 1, 2 were 0 failures after 20 drops whereas for comparative sample was 10 failures out of 20 drops. 

1. A heat shrinkable film comprising a heat sealing layer comprising an olefin block polymer.
 2. The heat shrinkable film of claim 1, wherein the olefin block polymer is an ethylene olefin block copolymer.
 3. The heat shrinkable film of claim 2, wherein the ethylene olefin block copolymer is an ethylene octene block copolymer having a melting point of more than 115° C.
 4. The heat shrinkable film of claim 1, wherein next to the heat sealing layer there is a layer comprising polypropylene.
 5. The film of claim 1, wherein the film comprises at least the heat sealing layer as an inner layer, a barrier layer and an outside layer.
 6. The film according to claim 1 or 5 where the film comprises an outside layer incorporating a polypropylene polymer an ethylene alpha olefin copolymer a styrene butadiene polymer a polyamide a polybutene or an EVOH polymer or a combination of one or more thereof.
 7. The film according to claim 1, 5 or 6 incorporating between the outside and barrier as well as between sealing and barrier further layers incorporating other polymers.
 8. The film according to claim 1 where the film is irradiated.
 9. The film according to claim 1 having a flat or tubular form.
 10. A bag or pouch made by the film of claim
 1. 11. A method of packaging and preserving a food product, comprising the steps of: a) providing a film as defined in claim 1 or a bag or pouch as defined in claim 10, and a food product; b) packaging the food product into said film, bag or pouch; c) subjecting the packaged food product to an elevated temperature for a predefined time thereby preserving the food product.
 12. The method of claim 11, wherein the elevated temperature is in a range of between about 70-98° C.
 13. The method of claim 11, wherein the time period for subjecting the packaged food product to an elevated temperature is between about 1 and 18 hours.
 14. The method of claim 11, wherein the packaged food product is subjected to an elevated temperature by immersing in hot water.
 15. A packaged food product obtainable by the method of claim
 11. 